WO2012041741A1 - Verfahren zur herstellung eines granulates enthaltend eines oder mehrere komplexbildnersalze - Google Patents
Verfahren zur herstellung eines granulates enthaltend eines oder mehrere komplexbildnersalze Download PDFInfo
- Publication number
- WO2012041741A1 WO2012041741A1 PCT/EP2011/066376 EP2011066376W WO2012041741A1 WO 2012041741 A1 WO2012041741 A1 WO 2012041741A1 EP 2011066376 W EP2011066376 W EP 2011066376W WO 2012041741 A1 WO2012041741 A1 WO 2012041741A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- jet
- jet apparatus
- zone
- complexing agent
- starting solution
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 29
- 239000008187 granular material Substances 0.000 title claims abstract description 25
- 150000003839 salts Chemical class 0.000 title claims abstract description 23
- 239000008139 complexing agent Substances 0.000 title claims abstract description 21
- 239000000243 solution Substances 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 19
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 12
- 239000007864 aqueous solution Substances 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 9
- 238000009472 formulation Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 6
- 150000002431 hydrogen Chemical class 0.000 claims description 6
- 230000033001 locomotion Effects 0.000 claims description 6
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 4
- 239000013618 particulate matter Substances 0.000 claims description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 3
- 229910052783 alkali metal Inorganic materials 0.000 claims description 3
- 150000001340 alkali metals Chemical class 0.000 claims description 3
- 150000003863 ammonium salts Chemical class 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 3
- 239000013042 solid detergent Substances 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 239000012459 cleaning agent Substances 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims description 2
- 239000000428 dust Substances 0.000 claims description 2
- 229910001385 heavy metal Inorganic materials 0.000 claims description 2
- 150000002500 ions Chemical class 0.000 claims description 2
- 239000003380 propellant Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 239000012530 fluid Substances 0.000 claims 1
- 239000007921 spray Substances 0.000 description 9
- 238000005469 granulation Methods 0.000 description 6
- 230000003179 granulation Effects 0.000 description 6
- MGFYIUFZLHCRTH-UHFFFAOYSA-N nitrilotriacetic acid Chemical class OC(=O)CN(CC(O)=O)CC(O)=O MGFYIUFZLHCRTH-UHFFFAOYSA-N 0.000 description 6
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000000543 intermediate Substances 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 238000005243 fluidization Methods 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- -1 methylglycine-N Chemical class 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- HRXKRNGNAMMEHJ-UHFFFAOYSA-K trisodium citrate Chemical compound [Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O HRXKRNGNAMMEHJ-UHFFFAOYSA-K 0.000 description 2
- OHOTVSOGTVKXEL-UHFFFAOYSA-K trisodium;2-[bis(carboxylatomethyl)amino]propanoate Chemical compound [Na+].[Na+].[Na+].[O-]C(=O)C(C)N(CC([O-])=O)CC([O-])=O OHOTVSOGTVKXEL-UHFFFAOYSA-K 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000234282 Allium Species 0.000 description 1
- 235000002732 Allium cepa var. cepa Nutrition 0.000 description 1
- 0 C*CN(C*)C* Chemical compound C*CN(C*)C* 0.000 description 1
- 101100001678 Emericella variicolor andM gene Proteins 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 238000005904 alkaline hydrolysis reaction Methods 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- OUDSFQBUEBFSPS-UHFFFAOYSA-N ethylenediaminetriacetic acid Chemical class OC(=O)CNCCN(CC(O)=O)CC(O)=O OUDSFQBUEBFSPS-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000005226 mechanical processes and functions Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 229920005646 polycarboxylate Polymers 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000002110 toxicologic effect Effects 0.000 description 1
- 231100000723 toxicological property Toxicity 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 238000010626 work up procedure Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C227/00—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
- C07C227/38—Separation; Purification; Stabilisation; Use of additives
- C07C227/40—Separation; Purification
- C07C227/42—Crystallisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/02—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops
- B01J2/06—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by dividing the liquid material into drops, e.g. by spraying, and solidifying the drops in a liquid medium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/16—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D11/00—Special methods for preparing compositions containing mixtures of detergents
- C11D11/0082—Special methods for preparing compositions containing mixtures of detergents one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/26—Organic compounds containing nitrogen
- C11D3/33—Amino carboxylic acids
Definitions
- the invention relates to a process for producing a granulate containing one or more complexing agent salts of the general formula I.
- aminopolyphosphonates, polycarboxylates or aminopolycarboxylates such as ethylenediaminetetraacetic acid (EDTA), which are frequently used as complexing agents, for example in detergents and cleaners, are only slightly biodegradable.
- EDTA ethylenediaminetetraacetic acid
- glycine-N, N-diacetic acid derivatives such as methylglycine-N, N-diacetic acid (MGDA) and its salts - e.g. the trialkali metal salts - which have beneficial toxicological properties and are readily biodegradable.
- MGDA methylglycine-N, N-diacetic acid
- salts e.g. the trialkali metal salts - which have beneficial toxicological properties and are readily biodegradable.
- the use of MGDA and related glycine-N, N-diacetic acid derivatives in detergents and their syntheses are e.g. in WO-A 94/029421 or US 5,849,950.
- For a cost-effective production of glycine-N, N-diacetic acid derivatives high demands are placed on the yield of the individual synthesis steps and purity of the isolated intermediates.
- MGDA is prepared in particular by reaction of iminodiacetonetril with acetaldehyde and hydrocyanic acid or of alpha-alanine nitrile with formaldehyde and hydrocyanic acid and alkaline hydrolysis of the intermediate methylglycinediacetontrile (MGDN) with sodium hydroxide solution, the trisodium salt of the MGDA being obtained.
- MGDN is generally isolated as an intermediate and used as a pure substance in the subsequent hydrolysis step.
- Complexing agent salts are often desired in coarse-grained form, because this is associated with many advantages, in particular with improved flow behavior, easier handling and improved meterability.
- a particularly advantageous process for producing coarse-grained products is the granulation in a special fluidized bed, the so-called spouted bed, also known as fluidized-bed spray granulation.
- the method is, for example, the subject of the diploma thesis of A. Werner: Wrbel layer spray granulation: process optimization in the spouted bed, September 2009, BASF SE and University of Stuttgart, Institute of Mechanical Process Engineering.
- the corresponding apparatuses are frequently referred to in the specialist and patent literature as spouted bed apparatus and are described, for example, in DE 10 2005 037 630, DE 10 162 781 or DE 103 22 062.
- the object of the invention was to provide a process for the preparation of granules of one or more complexing agent salts with improved space-time yield and improved product quality, in particular with a more compact, more uniform particle shape and with variables derived therefrom, in particular higher bulk density, lower fracture sensitivity and better flowability To make available.
- the object is achieved by a process for producing a granulate containing one or more complexing agent salts of the general formula
- n and m are each an integer from 0 to 5 and
- R '" is hydrogen or a C 1 -C 12 -alkyl radical or a C 2 -C 12 -alkenyl radical, which may additionally be substituted by up to 5 hydroxyl groups, or one of the groupings
- o and p are each an integer from 0 to 5
- M is independently of one another hydrogen, alkali metal, alkaline earth metal, ammonium or substituted ammonium in the corresponding stoichiometric amounts
- a jet apparatus in which a directed from bottom to top, centrally or one or more, positioned in the region of the central axis of the jet apparatus gaseous driving jet induce an internal loop movement, to form a jet zone, at the upper end of which a fountain zone connects, in a Return zone in the wall region of the jet apparatus passes, which merges again, in its lower part, in the jet zone, where the aqueous starting solution is injected into the one or more gaseous blowing jet and thereby dried to obtain the granules, which is discharged from the jet apparatus.
- the defined flow profile in the jet apparatus causes the forming granules to regularly pass the one or more nozzles via which the aqueous starting solution is sprayed, so that spraying is carried out regularly, at clearly defined time intervals. with the result that it comes to the regular growth of superimposed layers, in the manner of superimposed onion skins, and thus grow to very uniform particles.
- the granules obtained in this case have excellent product properties, in particular very high, defined bulk density, in the range between 650 and 1000 kg / m 3 , in particular between 760 and 920 kg / m 3 , and a defined, required for the purpose of residual moisture, in the range of about 6 to 14 wt .-% water, in particular 11 to 13 wt .-% water.
- an aqueous solution of one or more complexing agent salts with a concentration in the range of 10 to 80 wt .-%, based on the total weight of the aqueous solution.
- the aqueous starting solution may preferably be preheated to below the boiling point thereof.
- the one or more complexing agent salts correspond to the general formula
- n and m are each an integer from 0 to 5 and
- R '" is hydrogen or a C 1 -C 12 -alkyl radical or a C 2 -C 12 -alkenyl radical, which may additionally be substituted by up to 5 hydroxyl groups, or one of the groupings
- o and p are each an integer from 0 to 5
- M is independently hydrogen, alkali metal, alkaline earth metal, ammonium or substituted ammonium in the corresponding stoichiometric amounts.
- Alkali salts of methylglycine-N, N-diacetic acid are particularly preferred as derivatives of glycine-N, N-diacetic acid.
- aqueous starting solution is sucked into the propulsion jet of a jet apparatus, atomized by the jet and dried to obtain the granules, which is discharged in the upper part of the jet apparatus.
- fluidized-bed spray granulation is a shaping process for producing coarse-grained, monodisperse and almost round particles having particle sizes in the range between 0.3 mm and 30 mm, which are referred to herein as granules, starting from solutions, suspensions or melts.
- the Wrbel layer spray granulation is carried out in what is known as a spout layer, which is a special variant of a Wrbel layer.
- a spout layer which is a special variant of a Wrbel layer.
- particles are fluidized by introducing gas into a perforated bottom with a plurality of perforations (openings) from below Particle is blown collectively, wherein the particles are whirled up.
- the fluidization takes place via one or more few openings at the bottom of the jet apparatus, via which one or more blowing jets are injected.
- the one or more propulsion jets induce an internal, ordered loop motion, which may also be referred to as circular or cylindrical motion, and which comprises substantially three fluidization states or zones, a jet zone, a fountain zone, and a return zone.
- a first zone or jet zone the acceleration of the solid particles takes place under the action of the defined, guided from bottom to top propulsion jet, wherein the particles move in this zone in the flow direction of the propulsion jet. Accordingly, there is a vertical upward flow in the jet zone.
- a subsequent second zone or fountain zone the solid particles change their flow direction, there is a cross flow before.
- the particles enter a third zone or return zone in the wall region of the jet apparatus and there have a downward movement until they again reach the area of the, from the bottom upwards guided jet and in the first zone, the jet zone, again from Driving jet be entrained.
- the particles In the return zone, the particles typically move under the influence of gravity.
- a jet apparatus can preferably be used a cylindrical apparatus which tapers conically in the lower region thereof, by injecting a central propulsion jet from below.
- a propulsion jet apparatus of rectangular cross-section can be used, which tapers in a lower part, and in which in the region of the central axis of the same one or more driving beams from below are positioned upwards.
- a propulsion jet apparatus of rectangular cross-section can be used, which tapers in a lower part, and in which in the region of the central axis of the same one or more driving beams from below are positioned upwards.
- the one or more gaseous propulsion jets are formed from a gas which is under an overpressure in the range of 20 mbar to 1 bar above the pressure in the jet apparatus, which relaxes through an opening in the jet apparatus and thereby forms the gaseous propulsion jet.
- the propulsion jet is formed from a gas stream, which is preferably an inert gas, in particular air.
- crystalline particulate matter having a mean particle diameter in the range from about 1 to 100 ⁇ m, preferably from about 1 to 20 ⁇ m is added to the jet apparatus at a location separate from the aqueous starting solution , which is different from the point at which the aqueous starting solution is injected.
- the crystalline fine dust contains the same or the same complexing agent salts as are contained in the aqueous starting solution, or one or more complexing agent salts which are different therefrom.
- the gas stream forming the propulsion jet has a temperature in the range between 80 and 450 ° C, more preferably between 120 and 240 ° C.
- the temperature in the jet zone, in the fountain zone and in the return zone is preferably in the range between 70 and 150 ° C.
- the residence time in the jet apparatus is preferably between 1 minute and 1 hour, in particular between 10 minutes and 40 minutes.
- the invention also relates to formulations comprising the granules prepared by the process described above or aqueous solutions thereof as complexing agents for alkaline earth metal and heavy metal ions, in the amounts customary therefor, in addition to other conventional constituents of such formulations. These are preferably washing and cleaning agent formulations.
- the invention also relates to the use of the granules produced by the process described above for the production of press agglomerates.
- the press agglomerates are used in solid detergents, which are intended in particular for use in dishwashers.
- Example (according to the invention) A 40% strength aqueous Trilon M® solution (trisodium salt of methylglycine-N, N-diacetic acid) was spray-granulated in a jet apparatus of the type ProCell 5 from Glatt.
- the jet apparatus was operated with a volume flow of 180 NnfVh air of an inlet temperature of 180 ° C as propellant jet.
- 9.5 kg / h of the aqueous solution were sprayed into the lower area of the jet apparatus by means of a two-substance nozzle.
- As atomizing gas while compressed air was used at 8 bar.
- the temperature in the jet apparatus was 80 ° C.
- the granulation fluidized bed was operated with a volume flow of 205 NnfVh air at an inlet temperature of 160 ° C. 5.3 kg / h of the aqueous solution were sprayed with a two-component nozzle into the lower region of the granulating fluidized bed. In this case compressed air with 5 bar was used as sputtering gas. The temperature in the granulating fluidized bed was 100 ° C.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Detergent Compositions (AREA)
- Medicinal Preparation (AREA)
- Glanulating (AREA)
- Seasonings (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
MX2013003581A MX342570B (es) | 2010-09-27 | 2011-09-21 | Proceso para producir granulos que comprende una o mas sales de agentes complejantes. |
ES11758206.4T ES2547417T3 (es) | 2010-09-27 | 2011-09-21 | Procedimiento para la producción de un granulado que contiene una o varias sales de agentes complejantes |
CN201180046439.2A CN103124720B (zh) | 2010-09-27 | 2011-09-21 | 生产包含一种或多种络合剂盐的粒料的方法 |
CA2809749A CA2809749A1 (en) | 2010-09-27 | 2011-09-21 | Process for producing granules comprising one or more complexing agent salts |
EP11758206.4A EP2621892B1 (de) | 2010-09-27 | 2011-09-21 | Verfahren zur herstellung eines granulates enthaltend eines oder mehrere komplexbildnersalze |
KR1020137006511A KR101897991B1 (ko) | 2010-09-27 | 2011-09-21 | 하나 이상의 착화제 염을 포함하는 과립의 제조 방법 |
PL11758206T PL2621892T3 (pl) | 2010-09-27 | 2011-09-21 | Sposób wytwarzania granulatu zawierającego jedną lub większą liczbę soli kompleksotwórczych |
JP2013529639A JP5919278B2 (ja) | 2010-09-27 | 2011-09-21 | 1種以上の錯化剤塩を含有する顆粒の製造方法 |
RU2013119414/04A RU2573412C2 (ru) | 2010-09-27 | 2011-09-21 | Способ получения гранулята, содержащего одну или несколько солей комплексообразователя |
BR112013006404A BR112013006404A2 (pt) | 2010-09-27 | 2011-09-21 | processo para produzir grânulos, formulação, e, usos dos grânulos e dos aglomerados prensados |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP10180031 | 2010-09-27 | ||
EP10180031.6 | 2010-09-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2012041741A1 true WO2012041741A1 (de) | 2012-04-05 |
Family
ID=44654118
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2011/066376 WO2012041741A1 (de) | 2010-09-27 | 2011-09-21 | Verfahren zur herstellung eines granulates enthaltend eines oder mehrere komplexbildnersalze |
Country Status (12)
Country | Link |
---|---|
EP (1) | EP2621892B1 (ja) |
JP (1) | JP5919278B2 (ja) |
KR (1) | KR101897991B1 (ja) |
CN (1) | CN103124720B (ja) |
BR (1) | BR112013006404A2 (ja) |
CA (1) | CA2809749A1 (ja) |
ES (1) | ES2547417T3 (ja) |
MX (1) | MX342570B (ja) |
MY (1) | MY160461A (ja) |
PL (1) | PL2621892T3 (ja) |
RU (1) | RU2573412C2 (ja) |
WO (1) | WO2012041741A1 (ja) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017097657A1 (en) * | 2015-12-11 | 2017-06-15 | Basf Se | Process for manufacturing granules |
WO2020064379A1 (en) | 2018-09-27 | 2020-04-02 | Basf Se | Process for making a granule or powder |
WO2021115851A1 (en) | 2019-12-11 | 2021-06-17 | Basf Se | Granules of mgda and (meth)acrylic acid homo- or co-polymer; process for making the same |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11028350B2 (en) * | 2016-06-20 | 2021-06-08 | Basf Se | Powders and granules and process for making such powders and granules |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994029421A1 (de) | 1993-06-16 | 1994-12-22 | Basf Aktiengesellschaft | Verwendung von glycin-n,n-diessigsäure-derivaten als biologisch abbaubare komplexbildner für erdalkali- und schwermetallionen und verfahren zu deren herstellung |
EP0845456A2 (de) | 1996-11-29 | 1998-06-03 | Basf Aktiengesellschaft | Verfahren zur Herstellung eines kristallinen Feststoffes aus Glycin-N,N-diessigsäure-Derivaten mit hinreichend geringer Hygroskopizität |
US5849950A (en) | 1995-05-29 | 1998-12-15 | Basf Aktiengesellschaft | Preparation of glycine-N,N-diacetic acid derivatives |
DE10162781A1 (de) | 2001-12-20 | 2003-07-03 | Glatt Ingtech Gmbh | Strahlschichtapparat zur chargenweisen oder kontinuierlichen Prozessführung und Verfahren zum Betreiben eines Strahlschichtapparates |
DE10322062A1 (de) | 2003-05-15 | 2004-12-02 | Glatt Ingenieurtechnik Gmbh | Verfahren und Vorrichtung zum Aufbringen von Flüssigkeiten in eine Feststoffströmung eines Strahlschichtapparates |
WO2006120129A1 (de) | 2005-05-06 | 2006-11-16 | Basf Aktiengesellschaft | Verfahren zur herstellung von nebenproduktarmen methylglycin-n,n-diessigsäure-trialkalimetallsalzen |
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PT1638678E (pt) * | 2003-06-11 | 2012-01-05 | Glatt Ingtech Gmbh | Método para produção de granulados enzimáticos e granulados enzimáticos assim obtidos |
DE102005037750A1 (de) * | 2005-08-10 | 2007-02-22 | Glatt Ingenieurtechnik Gmbh | Verfahren zur Herstellung von Harnstoffpellets |
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- 2011-09-21 BR BR112013006404A patent/BR112013006404A2/pt active Search and Examination
- 2011-09-21 CN CN201180046439.2A patent/CN103124720B/zh active Active
- 2011-09-21 MX MX2013003581A patent/MX342570B/es active IP Right Grant
- 2011-09-21 PL PL11758206T patent/PL2621892T3/pl unknown
- 2011-09-21 EP EP11758206.4A patent/EP2621892B1/de active Active
- 2011-09-21 WO PCT/EP2011/066376 patent/WO2012041741A1/de active Application Filing
- 2011-09-21 KR KR1020137006511A patent/KR101897991B1/ko active IP Right Grant
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- 2011-09-21 CA CA2809749A patent/CA2809749A1/en not_active Abandoned
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Cited By (5)
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WO2017097657A1 (en) * | 2015-12-11 | 2017-06-15 | Basf Se | Process for manufacturing granules |
US10975334B2 (en) | 2015-12-11 | 2021-04-13 | Basf Se | Process for manufacturing granules |
WO2020064379A1 (en) | 2018-09-27 | 2020-04-02 | Basf Se | Process for making a granule or powder |
US12006487B2 (en) | 2018-09-27 | 2024-06-11 | Basf Se | Process for making a granule or powder |
WO2021115851A1 (en) | 2019-12-11 | 2021-06-17 | Basf Se | Granules of mgda and (meth)acrylic acid homo- or co-polymer; process for making the same |
Also Published As
Publication number | Publication date |
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JP2013544901A (ja) | 2013-12-19 |
KR20130106819A (ko) | 2013-09-30 |
JP5919278B2 (ja) | 2016-05-18 |
CA2809749A1 (en) | 2012-04-05 |
CN103124720A (zh) | 2013-05-29 |
RU2573412C2 (ru) | 2016-01-20 |
MX342570B (es) | 2016-10-05 |
EP2621892B1 (de) | 2015-07-29 |
RU2013119414A (ru) | 2014-11-10 |
ES2547417T3 (es) | 2015-10-06 |
MY160461A (en) | 2017-03-15 |
EP2621892A1 (de) | 2013-08-07 |
CN103124720B (zh) | 2014-12-10 |
MX2013003581A (es) | 2013-05-31 |
KR101897991B1 (ko) | 2018-09-12 |
PL2621892T3 (pl) | 2015-12-31 |
BR112013006404A2 (pt) | 2016-07-05 |
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